DNA encoding novel enzyme having D-serine synthase activity, method of producing the enzyme and method of producing D-serine by using the same

ABSTRACT

This invention relates to DNA encoding a novel enzyme having activity of synthesizing D-serine from formaldehyde and glycine, recombinant DNA constructed by integrating such DNA into a vector, a transformant transformed with the recombinant DNA, and a method for producing D-serine from formaldehyde and glycine with the use of the enzyme.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. patent application Ser. No. 13/034,098, filed on Feb. 24, 2011, issued as U.S. Pat. No. 9,211,376, which is a divisional application of U.S. patent application Ser. No. 11/665,194, filed on Apr. 12, 2007, issued as U.S. Pat. No. 7,919,285 which is a U.S. National Stage Application pursuant to 35 U.S.C. §371 of International Patent Application PCT/JP2005/18906, filed on Oct. 7, 2005.

TECHNICAL FIELD

The present invention relates to DNA encoding a novel enzyme having activity of synthesizing D-serine from formaldehyde and glycine, recombinant DNA constructed by integrating such DNA into a vector, a transformant transformed with the recombinant DNA, a novel enzyme having activity of synthesizing D-serine from formaldehyde and glycine, and a method for producing D-serine from formaldehyde and glycine with the use of the enzyme.

BACKGROUND ART

D-serine has been known as a compound that is useful as a synthesis intermediate for medicaments such as D-cycloserine.

Hitherto, as an enzyme having activity of synthesizing D-serine from formaldehyde and glycine, only D-threonine aldolase (hereafter to be abbreviated as “DTA”), which is derived from Arthrobacter sp. DK-19, has been known (JP Patent Publication (Kokai) No. 58-116690 A (1983)).

With the use of such DTA, it has been reported that the amount of D-serine produced was 2.5 mmol when 50 mmol each of formaldehyde and glycine were subjected to reaction at 30° C. for 40 hours. (The yield relative to formaldehyde was merely 5%.)

Meanwhile, it has been reported that DTA derived from Arthrobacter sp. DK-38, which is a microorganism of the same genus Arthrobacter, has a broad substrate specificity that responds to D-threonine, D-β-hydroxyphenylserine, D-β-hydroxy-α-aminovaleric acid, and the like; however, it does not react with D-serine (see Eur. J. Biochem., 1997, 248, pp. 385-393).

In addition, it has been reported that D-β-hydroxyamino acids can be produced from glycine and an aldehyde compound with the use of DTA derived from the genus Xanthomonas (JP Patent Publication (Kokai) No. 5-168484 A (1993)). However, it has not been reported that D-serine can be synthesized from formaldehyde and glycine with the use of DTA derived from the genus Xanthomonas.

DISCLOSURE OF THE INVENTION

In view of the aforementioned background art, it is an objective of the present invention to provide DNA encoding a novel enzyme having activity of synthesizing D-serine from formaldehyde and glycine, a recombinant DNA constructed by integrating such DNA into a vector, a transformant transformed with the recombinant DNA, a novel enzyme having an activity of synthesizing D-serine from formaldehyde and glycine, and a method for producing D-serine from formaldehyde and glycine with the use of the enzyme.

The present inventors thought that some unknown enzymes that have structures similar to those of known DTAs could be capable of synthesizing D-serine from formaldehyde and glycine. Thus, they examined information regarding the amino acid sequences of known DTAs. Accordingly, they have found information regarding the amino acid sequences of DTAs derived from the genera Xanthomonas (GenBank accession No. E05055), Achromobacter (GenBank accession No. AB026892), and Arthrobacter (GenBank accession No. AB010956). As a result of comparison and examination of these amino acid sequences, they have found that amino acid sequences corresponding to the N-terminal region and the C-terminal region of DTA are highly homologous to each other.

The present inventors designed primers based on these amino acid sequences of the N-terminal region and the C-terminal region. They then tried to amplify chromosome DNAs of a variety of microorganisms by PCR using the primers. Accordingly, they have succeeded in amplifying DNA encoding an enzyme having activity of synthesizing D-serine from formaldehyde and glycine with the use of a microorganism of the genus Achromobacter.

The amino acid sequence corresponding to the DNA is approximately 50% homologous to the amino acid sequence of known DTA derived from the genus Achromobacter, such that it significantly differs from the amino acid sequence of known DTA derived from the genus Achromobacter. Meanwhile, it is approximately 90% homologous to the amino acid sequence of known DTA derived from the genus Xanthomonas.

Next, the present inventors tried to synthesize D-serine by allowing formaldehyde to react with glycine using recombinant Escherichia coli that had been transformed with a recombinant DNA constructed by integrating the above novel DNA into a vector. Surprisingly, unlike the case of conventionally known DTA, they have found that D-serine can be synthesized with a reaction yield of as high as 70% or more from 100 mM glycine and 100 mM formaldehyde.

Further, when a D-serine accumulation reaction was carried out using the recombinant Escherichia coli, a small amount of L-serine was found to be produced.

When D-serine is used in a field in which it is necessary for medicine intermediates or the like to have high purity, it is not preferable that L-serine be mixed in D-serine. Formation of L-serine as a byproduct upon production of D-serine causes a significantly lowered purification yield of D-serine, since the solubility of DL-serine is lower than that of D-serine.

As a result of further examination to solve the above problems, the present inventors have found that formation of L-serine as a byproduct can be restrained by carrying out organic solvent treatment and/or heat treatment in the presence of divalent metal ions. In addition, they have found that, even without carrying out such treatment, formation of L-serine as a byproduct can be restrained by maintaining formaldehyde concentration at 150 mM or more during reaction. Furthermore, they have found that formation of L-serine as a byproduct can be restrained by using a microorganism lacking an L-serine synthase gene as a host producing DSA that is used for D-serine synthesis.

Based on the above findings, the present invention has been completed. Specifically, the present invention is as follows.

(1) DNA encoding a protein described in the following (a) or (b):

(a) a protein comprising an amino acid sequence set forth in SEQ ID NO: 4, 6, or 8; or

(b) a protein comprising an amino acid sequence derived from the amino acid sequence of (a) by deletion, substitution, insertion, or addition of one to several amino acid residues and having enzyme activity of synthesizing D-serine from glycine and formaldehyde.

(2) DNA described in the following (a) or (b):

(a) DNA comprising a nucleotide sequence set forth in SEQ ID NO: 3, 5, or 7 in the Sequence Listing or a sequence complementary to the nucleotide sequence; or

(b) DNA hybridizing under stringent conditions with a DNA fragment comprising a DNA sequence comprising at least 20 consecutive bases of the nucleotide sequence set forth in SEQ ID NO: 3, 5, or 7 in the Sequence Listing or of a sequence complementary to the nucleotide sequence and encoding an enzyme having an activity of synthesizing D-serine from glycine and formaldehyde.

(3) A recombinant DNA constructed by integrating the DNA described in (1) or (2) above into a vector.

(4) A transformant obtained by transforming a host cell using the recombinant DNA described in (3) above.

(5) The transformant described in (4) above, wherein the host cell to be transformed is a microorganism.

(6) The transformant described in (5) above, wherein the microorganism to be transformed is a D-serine-deaminase-deficient microorganism.

(7) A protein described in the following (a) or (b):

(a) a protein comprising an amino acid sequence set forth in SEQ ID NO: 4, 6, or 8; or

(b) a protein comprising an amino acid sequence derived from the amino acid sequence of (a) by deletion, substitution, insertion, or addition of one to several amino acid residues and having an enzyme activity of synthesizing D-serine from glycine and formaldehyde.

(8) A method for producing an enzyme having activity of synthesizing D-serine from glycine and formaldehyde, wherein the transformant described in any one of (4) to (6) above is cultured such that a protein having enzyme activity of synthesizing D-serine from glycine and formaldehyde is collected from the obtained culture product.

(9) A method for producing D-serine, comprising allowing glycine to react with formaldehyde in the presence of the transformant described in any one of (4) to (6) above or a treated product thereof.

(10) A method for producing D-serine, comprising allowing glycine to react with formaldehyde in the presence of the protein described in (7) above.

(11) A method for producing D-serine, wherein D-serine is synthesized by allowing glycine to react with formaldehyde in the presence of a microorganism having activity of synthesizing D-serine from glycine and formaldehyde or a treated product thereof, comprising one or more means described in the following (i) to (iv) whereby formation of L-serine as a byproduct in a reaction solution is restrained in a manner such that L-serine accounts for 1.5 mol % or less relative to D-serine during the reaction:

(i) a method for allowing a microorganism having activity of synthesizing D-serine from glycine and formaldehyde to be subjected to an organic solvent treatment and/or heat treatment;

(ii) a method for controlling formaldehyde concentration in a reaction solution a) to 2M or less in a case in which an organic solvent treatment and/or heat treatment are/is carried out by the method (i) above and b) to from 150 mM to 2M inclusive in a case in which an organic solvent treatment and/or heat treatment are/is not carried out;

(iii) a method for using, as a catalyst, a microorganism comprising an enzyme having activity of synthesizing D-serine from glycine and formaldehyde and lacking a L-serine synthase gene; and

(iv) a method for adding a microorganism comprising an enzyme having an L-serine deaminase activity to a reaction solution.

(12) The production method described in (11) above, wherein the organic solvent is at least one selected from the group consisting of formaldehyde, benzaldehyde, dichloroethane, and isopropyl alcohol.

(13) The production method described in (11) or (12) above, wherein the organic solvent treatment and/or heat treatment are/is carried out in the presence of divalent metal ions.

(14) The production method described in (13) above, wherein the divalent metals are one or more types of metals selected from the group consisting of magnesium, manganese, zinc, nickel, cobalt, and iron.

(15) The production method described in (11) above, wherein the microorganism having activity of synthesizing D-serine from glycine and formaldehyde is the transformant described in (5) or (6) above.

1. Obtaining a Gene of DNA Encoding a Novel Enzyme Having Activity of Synthesizing D-Serine from Formaldehyde and Glycine

DNA comprising the amino acid sequence set forth in SEQ ID NO: 4, 6, or 8 in the Sequence Listing and encoding an enzyme having activity of synthesizing D-serine from glycine and formaldehyde (hereafter to be abbreviated as “DSA”) can be obtained by extracting chromosomal DNA from, for example, Achromobacter xylosoxidans (ATCC9220), which is available from the American Type Culture Collection (12301 Parklawn Drive, Rockville, Md. 20852, U.S.A.), and Achromobacter xylosoxidans (NBRC13495) and Achromobacter denitrificans (Synonym: Achromobacter xylosoxidans subsp. denitrificans) (NBRC15125), which are available from the NITE Biological Resource Center of the National Institute of Technology and Evaluation (2-5-8 Kazusakamatari, Kisarazu-shi, Chiba, Japan) and carrying out PCR with the use of primers comprising the nucleotide sequences set forth in SEQ ID NOS: 1 and 2 in the Sequence Listing, respectively.

It is effective to improve amplification conditions in a manner such that a gene having a few mismatched bases can be amplified when carrying out PCR. For instance, a gene that is amplified with difficulty can be occasionally amplified by a method wherein the annealing temperature is controlled at a low temperature, by a method involving the addition of dimethyl sulfoxide (approximately 5%) to a PCR reaction solution, by a method using a PCR kit (e.g., GC-RICH PCR System produced by Roche) that is designed to readily amplify a GC-rich gene, or by a combination of the above methods or the like.

Specific examples of DNA encoding DSA include the DNA nucleotide sequence of a DTA gene derived from Achromobacter xylosoxidans (ATCC9220) set forth in SEQ ID NO: 3, the amino acid sequence (translated by such nucleotide sequence) set forth in SEQ ID NO: 4, the DNA nucleotide sequence of a DTA gene derived from Achromobacter xylosoxidans (NBRC13495) set forth in SEQ ID NO: 5, the amino acid sequence (translated by such nucleotide sequence) set forth in SEQ ID NO: 6, the DNA nucleotide sequence of a DTA gene derived from Achromobacter denitrificans (NBRC15125) set forth in SEQ ID NO: 7, and the amino acid sequence (translated by such nucleotide sequence) set forth in SEQ ID NO: 8.

In addition to the aforementioned DNAs encoding DSA, DNA encoding DSA may be derived from any types of organisms, as long as it hybridizes with a DNA fragment comprising a DNA sequence of at least 20 consecutive bases of the nucleotide sequence set forth in SEQ ID NO: 3, 5, or 7 in the Sequence Listing or of a sequence complementary to such nucleotide sequence under stringent conditions and it encodes a protein having DSA activity. For instance, even a silent DNA that does not function in an organism may be used as long as it can produce DSA by ligating such DNA that has been isolated to an adequate expression vector.

Further, even if no organism is specified, DNA encoding DSA can be obtained by allowing soil or the like that is used for template DNA to be directly subjected to PCR using the primers having the nucleotide sequences set forth in SEQ ID NOS: 1 and 2 in the Sequence Listing.

A specific example of DNA encoding DSA is obtained by a method wherein PCR is carried out using, for example, chromosome DNA of a microorganism that grows in a medium containing D-serine as a template and primers having the nucleotide sequences set forth in SEQ ID NOS: 1 and 2 in the Sequence Listing, such that DNA is amplified.

In addition, it is also possible to obtain DNA encoding a protein having DSA activity and comprising an amino acid sequence derived from the amino acid sequence set forth in SEQ ID NO: 4, 6, or 8 by deletion, substitution, insertion, or addition of one to several amino acid residues via introduction of adequate mutation such as deletion, substitution, insertion, and/or addition with the use of site-specific mutagenesis methods (Nucleic Acid Res., 10, p. 6487 (1982); Nucleic Acid Res., 13, p. 4431 (1985); Methods in Enzymol., 100, p. 448 (1983); Molecular Cloning 2^(nd) Ed., Cold Spring Harbor Laboratory Press (1989); PCR A Practical Approach IRL Press p. 200 (1991); Current Protocols in Molecular Biology, John Wiley & Sons (1987-1997); Proc. Natl. Acad. Sci., USA, 79, p. 6409 (1982); Gene, 34, 315 (1985); and Proc. Natl. Acad. Sci., USA, 82, p. 488 (1985)) or the like, as long as the nucleotide sequence set forth in SEQ ID NO: 3, 5, or 7 in the Sequence Listing or a sequence complementary thereto can hybridize under stringent conditions and such mutation does not influence the activity of the enzyme to be encoded.

Deletion, substitution, insertion, or addition of amino acid residues described herein can be carried out by the aforementioned site-specific mutagenesis methods that were known techniques prior to the filing of the present application. In addition, the term “one to several amino acid residues” indicates a number of amino acids that allows deletion, substitution, insertion, or addition of amino acid residues (for example, 1 to 5 amino acid residues and preferably 1 to 3 amino acid residues) to be carried out by site-specific mutagenesis methods.

Examples of conditions for hybridization include conditions that are generally used by persons skilled in the art to detect particular hybridization signals. Preferably, such conditions indicate stringent hybridization conditions and stringent washing conditions. Specifically, for instance, such conditions involve overnight incubation at 55° C. with the use of a probe in a solution containing 6×SSC (1×SSC composition: 0.15 M NaCl and 0.015 M sodium citrate (pH 7.0)), 0.5% SDS, 5×Denhardt's solution, and 100 mg/ml herring sperm DNA. Such conditions also involve washing of a filter in 0.2×SSC at 42° C. Stringent conditions involve a use of 0.1×SSC at 50° C. during a step of washing a filter. As a further stringent condition, a condition using 0.1×SSC at 65° C. during the same step can be explained.

The phrase “a DNA fragment comprising a DNA sequence comprising at least 20 consecutive bases of the nucleotide sequence set forth in SEQ ID NO: 3, 5, or 7 or of a sequence complementary to such nucleotide sequence” used herein indicates a DNA fragment obtained by choosing one or more sequence comprising at least 20 and preferably at least 30 (e.g., 40, 60, or 100) arbitrary consecutive bases of the sequence set forth in SEQ ID NO: 3, 5, or 7 in the Sequence Listing or of a sequence complementary to such sequence.

2. Production of a Recombinant DNA Having the Gene of the Protein

A recombinant DNA can be obtained by integrating the aforementioned DNA encoding DSA into a vector.

A vector that is appropriate for cloning is a vector that is constructed for gene recombination with the use of a phage or plasmid that is capable of autonomously replicating in a host microorganism. For instance, when Escherichia coli is a host microorganism, examples of such phage include Lambda gt10 and Lambda gt11. In addition, for instance, when Escherichia coli is a host microorganism, examples of such plasmid include pBTrp2, pBTac1, and pBTac2 (produced by Boehringer Mannheim), pKK233-2 (produced by Pharmacia), pSE280 (produced by Invitrogen), pGEMEX-1 (produced by Promega), pQE-8 (produced by QIAGEN), pQE-30 (produced by QIAGEN), pBluescriptII SK+ and pBluescriptII SK(−) (produced by Stratagene), pET-3 (produced by Novagen), pUC18 (produced by Takara Shuzo Co., Ltd.), pSTV28 (produced by Takara Shuzo Co., Ltd.), pSTV29 (produced by Takara Shuzo Co., Ltd.), and pUC118 (produced by Takara Shuzo Co., Ltd.).

As such promoter, any promoter may be used as long as it can be expressed in a host cell. Examples thereof include promoters derived from Escherichia coli, phages, or the like, such as a trp promoter (P_(trp)), a lac promoter (P_(lac)), a P_(L) promoter, a P_(H) promoter, and a P_(SE) promoter. In addition, promoters and the like that are artificially designed and modified, such as a tac promoter and a lacT7 promoter, can be used. Further, in order to cause expression in bacteria of the genus Bacillus, it is also possible to use an Np promoter (JP Patent Publication (Kokoku) No. 8-24586 B (1996)).

As a ribosome binding sequence, any sequence can be used as long as it can be expressed in a host cell. However, it is preferable to use a plasmid in which a Shine-Dalgarno sequence and an initiation codon are adjusted to have an adequate distance (e.g., 6 to 18 bases) therebetween.

In order to efficiently carry out transcription and translation, a protein, in which the N-terminal of a protein having activity of the protein or a protein derived from such a protein by deletion of a portion thereof is fused with the N-terminal of a protein encoded by an expression vector, may be expressed.

A transcription termination sequence is not always necessary for the expression of a protein of interest. However, it is preferable to place a transcription termination sequence directly below a structural gene.

Upon cloning, it is possible to obtain a vector fragment by cleaving a vector as described above with a restriction enzyme used for cleavage of the aforementioned DNA encoding DSA. However, the same restriction enzyme used for cleavage of the DNA is not necessarily used. A method for binding the DNA fragment and a vector DNA fragment may be used as long as a known DNA ligase is used in such a method. For instance, after annealing of a cohesive end of the DNA fragment and that of a vector fragment, a recombinant vector of the DNA fragment and the vector DNA fragment is produced with the use of an adequate DNA ligase. Also, it is possible to produce a recombinant vector by transferring the resultant of such annealing into a host such as a microorganism and using an in vivo DNA ligase according to need.

3. Production of a Transformant Using a Recombinant DNA Constructed by Integrating DNA Encoding DSA into a Vector

A transformant transformed with the aforementioned recombinant DNA can be obtained by introducing the aforementioned recombinant DNA into a host cell.

As a host cell, there is no particular limitation, as long as a recombinant vector is stable and can autonomously replicate and a foreign gene is phenotypically expressed therein. Examples of such host cell include microorganisms such as bacteria, including Escherichia coli such as Escherichia coli DH5α and Escherichia coli XL-1Blue. In addition, it is possible to use other microorganisms such as yeasts or insect cells as host cells.

In a case in which a microorganism is Escherichia coli, for example, the method for transferring recombinant DNA into the microorganism that can be used is a competent cell method using calcium treatment, an electroporation method, or the like.

As a host cell, for the purpose of restraining degradation of D-serine as a product, it is possible to use a microorganism having low D-serine deaminase activity or a microorganism lacking D-serine deaminase activity. Specific examples of a microorganism lacking D-serine deaminase activity include Escherichia coli having a recombinant D-serine deaminase gene described in Example 6.

In addition, for the purpose of restraining production of L-serine during a D-serine synthesis reaction, it is possible to degrade L-serine produced using a microorganism having high L-serine deaminase activity. As a microorganism having high L-serine deaminase activity, Escherichia coli having a recombinant L-serine deaminase gene described in Example 15 or the like can be used.

As such microorganism, a microorganism having low activity of an enzyme involved in L-serine synthesis, such as alanine racemase, serine hydroxymethyltransferase, or L-threonine aldolase, or a microorganism lacking such enzyme activity is preferably used so that L-serine is not produced.

Further preferably, a microorganism lacking all of the above enzymes is used as a host cell.

4. Production of DSA

DSA can be produced by culturing the aforementioned transformant and collecting the thus obtained DSA.

A transformant can be cultured in accordance with a usual method used for culture of host cells. In a case in which a transformant is a procaryotic microorganism such as Escherichia coli or a eucaryotic microorganism such as a yeast, a medium in which such a microorganism is cultured may be a natural or synthetic medium as long as it contains carbon sources, nitrogen sources, inorganic salts, and the like, which cause assimilation of the microorganism, and as long as a transformant can efficiently be cultured therein.

Examples of carbon sources that can be used include: glucose, fructose, or sucrose; molasses containing any thereof; carbohydrates such as starch and starch hydrolysate; organic acids such as acetic acid and propionic acid; and alcohols such as ethanol and propanol, as long as they can cause assimilation of a transformant.

Examples of nitrogen sources that can be used include: ammonia; a variety of ammonium salts of inorganic or organic acid, such as ammonium chloride, ammonium sulfate, ammonium acetate, and ammonium phosphate; other nitrogen-containing compounds; peptone; meat extracts; yeast extracts; corn steep liquor; casein hydrolysate; soybean cake; soybean cake hydrolysate; and a variety of fermentation bacteria and digests thereof.

Examples of inorganic salts that can be used include monopotassium phosphate, dipotassium phosphate, magnesium phosphate, magnesium sulfate, sodium chloride, ferrous sulfate, manganese sulfate, copper sulfate, and calcium carbonate.

Culture is carried out under aerobic conditions used for shake culture, submerged cultivation under aeration and agitation, or the like. Culture temperature is preferably 15° C. to 50° C. Culture time is 16 hours to 5 days, in general. During culture, pH is maintained between 3.0 and 9.0. The pH is adjusted with the use of inorganic or organic acids, alkaline solutions, urea, calcium carbonate, ammonia, and the like. In addition, during culture, antibiotics such as ampicillin and tetracycline may be added to the medium according to need.

When a microorganism transformed with an expression vector in which an inducible promoter is used as a promoter is cultured, an inducer may be added to the medium according to need. For instance, when a microorganism transformed with an expression vector in which a lac promoter is used is cultured, isopropyl-β-D-thiogalactopyranoside (IPTG) or the like may be added to the medium. Also, when a microorganism transformed with an expression vector in which a trp promoter is used is cultured, indoleacetic acid (IAA) or the like may be added to the medium.

A transformant can be separated and recovered by means of centrifugation, filtration, or the like, of a culture solution containing the transformant.

A treated product of a transformant can be obtained by allowing the transformant to be subjected to mechanical disruption, ultrasonication, freezing and thawing treatment, drying treatment, pressurization or depressurization treatment, osmotic pressure treatment, autodigestion, surfactant treatment, or enzyme treatment for the purpose of cell disruption. Also, a treated product of a transformant can be obtained as an immobilized fraction or transformant, which comprises DSA obtained via such treatment.

In addition, the treated product of a microorganism of the present invention is also referred to as a product subjected to a treatment similar to that used for the aforementioned treated product of a transformant.

In order to purify DSA from such transformant or a treated product of such transformant, transformed cells are disrupted and a cell disruption solution is subjected to a combination of, for example, fractionation via ion-exchange resin or gel-filtration chromatography or the like and salting out with the use of ammonium sulfate or the like, such that a purified enzyme can be obtained.

5. Production of D-Serine

D-serine can be produced by allowing glycine to react with formaldehyde in the presence of the aforementioned transformant or a treated product of the transformant.

Production of D-serine is preferably carried out under conditions of shaking or agitation at pH 6.0 to 9.0 and at a temperature of 20° C. to 60° C.

The amount of transformant or treated product of the transformant used is not particularly limited, as long as the reaction between formaldehyde and glycine progresses well. In general, a transformant or a treated product of the transformant is preferably added in an amount of at least 10 units and preferably 50 units or more in terms of DSA activity relative to 1 g of glycine. In accordance with a method for adding the transformant or a treated product of the transformant, such transformant may be added at once upon the initiation of reaction, at several different times, or continuously throughout reaction.

Regarding DSA activity, capacity for synthesizing 1 μmol of D-serine per 1 minute is defined as 1 unit.

DSA activity is calculated by measuring the amount of D-serine that is produced in a manner such that an enzyme solution is added to 200 mM Tris-hydrochloric acid buffer (pH 8.0) containing 100 mM glycine, 0.1 mM pyridoxal phosphate, 10 mM magnesium chloride, and 5 mM formaldehyde, followed by incubation at 30° C.

Glycine concentration in a reaction solution is 100 mM or more and preferably between 1 M and 5 M. In accordance with a method for adding glycine, it may be added at once upon the initiation of reaction, at several different times, or continuously along with the progress of reaction.

It is possible to supply formaldehyde in the form of gas into a reaction solution. Also, it can be supplied in the form of an aqueous or alcohol solution. In addition, as a supply source of formaldehyde, paraformaldehyde can also be used. However, an aqueous solution of approximately 37% formaldehyde is preferably used.

As a method for adding formaldehyde, a method of adding formaldehyde at once or a method of adding formaldehyde at several different times or continuously along with the progress of reaction can be carried out. Preferably, formaldehyde concentration in a reaction solution is controlled at a concentration that allows DSA activity not to be inhibited. A concentration that allows DSA activity not to be inhibited is generally 5 M or less, preferably 2 M or less, further preferably 500 mM or less, and particularly preferably 300 mM or less.

Also, formaldehyde can be added by the following methods for controlling formaldehyde concentration in a reaction solution: (1) a method for adding formaldehyde in a reaction solution at a given rate; (2) a method wherein formaldehyde concentration is quantified such that formaldehyde is added at several different times at a concentration that allows enzyme activity not to be deactivated; (3) a method for substantially avoiding inhibition due to formaldehyde, wherein paraformaldehyde is added and an enzyme is added to a reaction system at a rate that exceeds the rate at which formaldehyde is released from paraformaldehyde; and (4) a method for adding formaldehyde in an amount at which an increased pH level can be corrected. In the case of (4) above, D-serine as a product accumulates in a reaction solution along with the progress of reaction, the amount of glycine as a starting material decreases, and the pH of a reaction solution decreases along with the progress of the reaction. This is because the isoelectric point of D-serine is 5.68 and that of glycine is 5.97, such that alkali is added to the reaction solution in an amount that exceeds an amount necessary for correction of a decrease in the pH of the reaction solution, resulting in an increased pH level.

When formaldehyde is added at a rate that exceeds the rate of adding alkali while the amount of DSA in a reaction solution is predetermined (that is to say, at a rate that exceeds the rate of D-serine synthesis), it becomes possible to control formaldehyde concentration in a reaction solution without using complicated operations such as measurement of formaldehyde concentration.

Examples of alkali that may be added to a reaction solution include: alkali metal hydroxide such as lithium hydroxide, sodium hydroxide, or potassium hydroxide; ammonium hydroxide; calcium hydroxide; dipotassium phosphate; disodium phosphate; potassium pyrophosphate; and ammonia, as long as it is dissolved in water such that basicity is imparted to the liquid.

A medium used for a reaction solution is water, an aqueous medium, an organic solvent, or a mixture solution of water or an aqueous medium and an organic solvent. Examples of an aqueous medium that is used include buffer solutions such as a phosphate buffer solution, a HEPES (N-2-hydroxyethylpiperazin-N-ethanesulfonic acid) buffer solution, and a Tris(Tris(hydroxymethyl)aminomethane) hydrochloric acid buffer solution. Examples of an organic solvent that may be used include any organic solvent such as acetone, ethyl acetate, dimethyl sulfoxide, xylene, methanol, ethanol, or butanol, unless it inhibits reaction.

In the aforementioned reaction, reaction yield may be improved with the addition of a compound having divalent metal ions, reductants such as 2-mercaptoethanol, dithiothreitol, and sodium bisulfite, and coenzymes such as pyridoxal phosphate and an ammonium salt.

Examples of a compound having divalent metal ions include magnesium chloride, manganese chloride, cobalt acetate, ferrous sulfate, and calcium chloride.

The concentration of such compound in a reaction solution is generally 0.1 mM to 100 mM and preferably 0.1 mM to 10 mM.

6. Method for Improving Optical Purity of D-Serine in a Reaction Solution

Formation of L-serine as a byproduct can be restrained by allowing glycine to react with formaldehyde in the presence of a treated product obtained by allowing the aforementioned transformant or a treated product of the transformant to be subjected to heat treatment or in the presence of a treated product obtained by allowing the aforementioned transformant or a treated product of the transformant to be subjected to organic solvent treatment.

As conditions of heat treatment, any conditions may be applied, provided that thereby DSA activity is not significantly reduced by heating and L-serin production activity can be reduced or eliminated. Specific examples of such treatment include a method of agitation at pH 6.0 to 9.0 at a temperature of 40° C. to 70° C. for 10 minutes to 6 hours.

In addition, organic solvent treatment and heat treatment can be used in combination.

As conditions of organic solvent treatment, any conditions may be applied, provided that thereby DSA activity is not significantly reduced and L-serin production activity can be reduced or eliminated. Such conditions of organic solvent treatment involve organic solvent concentration that is generally approximately between 20 mM and 2 M, preferably approximately between 20 mM and 1 M, further preferably approximately between 50 mM and 1000 mM, and particularly preferably approximately between 50 mM and 300 mM. Preferred examples of an organic solvent that is used include: aldehydes such as formaldehyde, acetaldehyde, and benzaldehyde; alcohols such as methanol, ethanol, and isopropyl alcohol; ketones such as acetone; and halogenated hydrocarbons such as dichloroethane. However, the organic solvent is not limited thereto unless it causes a significant decrease in DSA activity. Among them, formaldehyde is the most preferable because it is a substrate for enzyme reactions. Since the addition of D-serine results in production of formaldehyde during such enzyme reaction, a method for adding D-serine instead of formaldehyde may be implemented. It is desired that the concentration of D-serine added be approximately 100 mM to 5 M.

It is desired that the temperature for organic solvent treatment be between 10° C. and 50° C. and that the pH for the treatment be between 6.0 and 9.0. During organic solvent treatment, agitation is desirably carried out such that the pH and the organic solvent concentration become uniform in a treatment solution.

In addition, upon the initiation of reaction of D-serine production, it is possible to reduce or deactivate L-serine production activity by increasing formaldehyde concentration. In such case, formaldehyde concentration during reaction is maintained at approximately 0.1% to 5% for 30 minutes to 3 hours and then a general reaction may be carried out.

When carrying out the aforementioned treatment, enzyme activity may be further stabilized by adding a compound having divalent metal ions, reductants such as 2-mercaptoethanol, dithiothreitol, and sodium bisulfite, and coenzymes such as pyridoxal phosphate and an ammonium salt.

Examples of a compound having divalent metal ions include magnesium chloride, manganese chloride, cobalt acetate, ferrous sulfate, and calcium chloride.

A concentration of such compound in a treatment solution is generally 0.1 mM to 100 mM and preferably 0.1 mM to 10 mM.

It is also possible to improve optical purity of D-serine as a final product by adding L-serine-deaminase-producing bacteria to a reaction solution after the termination of a D-serine synthesis reaction so as to degrade the L-serine produced. As L-serine deaminase-producing bacteria, microorganisms lacking D-serine deaminase are desirably used.

7. Method for Collecting D-Serine

D-serine can be collected from a reaction solution in accordance with methods that are used in general organic synthetic chemistry, such as extraction using organic solvents, crystallization, thin-layer chromatography, and high-performance liquid chromatography.

In accordance with the present invention, D-serine can be produced from glycine and formaldehyde with a better yield than is possible with methods for producing D-serine using known DTAs.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows the results of SDS-polyacrylamide gel electrophoresis analysis of a cell disruption solution obtained from transformants.

FIG. 2 shows an SDS-polyacrylamide gel electrophoresis image of purified DSA.

This description includes part or all of the contents as disclosed in the description and/or drawings of Japanese Patent Application No. 2004-298344, which is a priority document of the present application.

BEST MODE FOR CARRYING OUT THE INVENTION

Examples of the present invention will hereafter be described. However, the technical scope of the present invention is not limited to the Examples. In addition, D-serine, L-serine, and glycine were quantified by high-performance liquid chromatography. Conditions for analyzing them and a method for measuring activities of enzymes (DSA and DTA) were as follows.

(1) Conditions for Analyzing D-Serine and L-Serine

Column: TSK-GEL ENANTIO L1 4.6×250 (Tosoh Corporation)

Column temperature: 45° C.

Pump flow rate: 0.8 ml/min.

Detection: UV 254 nm

Eluent: 0.25 mM copper sulfate: methanol=9:1 (v/v)

(2) Conditions for Analyzing Serine and Glycine

Column: Shodex RSpak NN-814 8×250 (Showa Denko K.K.)

Column temperature: 40° C.

Eluent: 10 mM potassium phosphate (pH 3.0)

Pump flow rate: 0.8 ml/min

Detection was carried out by a post-column derivatization method (J. Chromatogr., 83, 353-355 (1973)) using orthophthalaldehyde (OPA).

(3) A Method for Measuring Enzyme Activity

An enzyme solution that had been obtained by allowing a cell suspension to be subjected to ultrasonic disruption was adequately diluted. The diluted enzyme solution (0.1 mL) was added to 0.9 mL of 200 mM Tris-hydrochloric acid buffer (pH 8.0) containing 100 mM glycine, 0.1 mM pyridoxal phosphate, 10 mM magnesium chloride, and 5 mM formaldehyde. The resulting solution was subjected to reaction at 30° C. for 15 minutes.

D-serine produced was analyzed by HPLC so as to measure the activity. Herein, 1 unit of such activity was determined to be the capacity for producing 1 μmol of D-serine per 1 minute.

Example 1

(Obtaining the Gene Encoding DSA)

An LB medium (50 ml) was inoculated with Achromobacter xylosoxidans (ATCC9220), Achromobacter denitrificans (NBRC15125), and Achromobacter xylosoxidans (NBRC13495). After overnight culture at 30° C., harvest was carried out, followed by bacteriolysis using a lytic solution containing lysozyme (1 mg/ml). The resulting lysate was subjected to phenol treatment. Then, DNA was allowed to precipitate by ethanol precipitation in accordance with a usual method. The resulting DNA precipitate was recovered by spooling it onto a glass rod and washed so as to be used for PCR.

Primers used for PCR were oligonucleotides (obtained by custom synthesis from Hokkaido System Science Co., Ltd.) having the nucleotide sequences set forth in SEQ ID NOS: 1 and 2, respectively, which were designed based on known DTA genes. These primers had KpnI and HindIII restriction enzyme recognition sequences near the 5′ and 3′ ends, respectively.

With the use of 0.025 ml of a PCR reaction solution containing 6 ng/μl each of chromosome DNAs of the aforementioned microorganisms and 3 μM each of the primers, PCR was carried out under the following conditions: denaturation at 96° C. for 1 minute, annealing at 55° C. for 30 seconds, and elongation reaction at 68° C. for 1 minute and 15 seconds for 35 reaction cycles.

The PCR reaction product and plasmid pUC18 (Takara Shuzo) were digested with KpnI and HindIII, followed by ligation using Ligation High (TOYOBO). Thereafter, the obtained recombinant plasmid was used for transformation of Escherichia coli DH5α. The transformed cell line was cultured in an LB agar medium containing 50 μg/ml of ampicillin (Am) and X-Gal (5-bromo-4-chloro-3-indolyl-β-D-galactoside). Thus, an Am-resistant transformed cell line that was formed into a white colony was obtained. A plasmid was extracted from the thus obtained transformed cell line. The nucleotide sequence of the DNA fragment that had been introduced into the plasmid was confirmed in accordance with a usual method for base sequencing.

Molecular weights of amino acid sequences that were expected based on the obtained DNAs encoding DSA were approximately 40 kDa each.

The obtained plasmid having DNA encoding DSA derived from Achromobacter xylosoxidans (ATCC9220) was designated as pAcDTA1.

The plasmid having DNA encoding DSA derived from Achromobacter xylosoxidans (NBRC13495) was designated as pAcDTA2. The plasmid having DNA encoding DSA derived from Achromobacter denitrificans (NBRC15125) was designated as pAcDTA3.

(Production of Transformants)

Escherichia coli DH5α was transformed by a usual method using pAcDTA1, pAcDTA2, and pAcDTA3. The obtained transformants were designated as MT-11015, MT-11016, and MT-11017, respectively.

A LB medium (100 mL) containing 50 μg/ml of Am was inoculated with recombinant microorganisms of each transformant after being placed in a 500-mL baffled Erlenmeyer flask. This was followed by culture at 30° C. until OD660 reached 0.6. Then, IPTG (isopropyl-3-thiogalactopyranoside) was added thereto such that the medium contained 1 mM IPTG. This was followed by further shake culture for 16 hours. The culture solution was centrifuged at 13000 rpm for 10 minutes. The obtained cell bodies were suspended in 100 mM Tris-hydrochloric acid buffer (pH 8.0) containing 5 mL of 1 mM magnesium chloride, followed by cryopreservation at −20° C.

Example 2

(Method for Producing DSA)

Suspensions (0.5 mL each) of the transformants produced in Example 1 were disrupted using a Bioruptor (produced by Olympus) in ice water for 5 minutes. A transformant disruption solution was centrifuged such that the transformant disruption solution was prepared. FIG. 1 shows the results of SDS-polyacrylamide gel electrophoresis analysis of the transformant disruption solution.

0.5 mL of 100 mM Tris-hydrochloric acid buffer (pH 8.0) was added to the precipitate so as to obtain cell residue, followed by analysis in a similar manner.

In a soluble fraction of each transformant, a protein that was expressed at a position of 40 kDa was found. However, such protein was not found in an insoluble fraction. The molecular weight of the protein was almost equivalent to the molecular weight of an amino acid sequence that was based on the corresponding gene.

Example 3

(Purification of DSA and D-Serine Synthesis with the Use of Purified DSA)

10 mL of a MT-11015 disruption solution produced in a manner similar to that used in Example 2 was centrifuged at 10000 rpm for 20 minutes such that an enzyme solution was prepared, and cell residue was then removed therefrom. The enzyme solution was allowed to adsorb anion exchange resin (HiTrap Q-XL produced by Amersham), followed by linear-gradient elution from 100 mM Tris-hydrochloric acid buffer (pH 8.0) containing 10 mM magnesium chloride and 50 mM sodium chloride to 100 mM Tris-hydrochloric acid buffer (pH 8.0) containing 10 mM magnesium chloride and 500 mM sodium chloride. The activity fraction was allowed to adsorb hydrophobic chromatography resin (HiTrap Phenyl FF produced by Amersham), followed by linear-gradient elution from 100 mM Tris-hydrochloric acid buffer (pH 8.0) containing 10 mM magnesium chloride, which had been saturated with ammonium sulfate, to 100 mM Tris-hydrochloric acid buffer (pH 8.0) containing 10 mM magnesium chloride. Note that the above operations were carried out at approximately 10° C.

FIG. 2 shows the results of SDS-polyacrylamide gel electrophoresis analysis of a solution subjected to ultrasonic disruption, an activity fraction subjected to ion-exchange chromatography treatment, and an activity fraction subjected to hydrophobic chromatography treatment. The molecular weight of purified DSA monomer was 40000±5000.

The purified DSA enzyme solution (150 units) was added to a substrate solution comprising 100 mM formaldehyde, 100 mM glycine, 0.1 mM PLP, 10 mM magnesium chloride, and 100 mL of 200 mM Tris-hydrochloric acid buffer (pH 8.0). The resultant was subjected to reaction at 30° C. for 20 hours.

The reaction yield of D-serine was 95%.

Example 4

(Comparison Between D-Serine Synthesis Capacity and D-Threonine Synthesis Capacity)

The enzyme solution subjected to ultrasonic disruption (150 units) of the cell line MT-11015 produced in Example 1 was added to a substrate solution comprising 100 mM formaldehyde or acetaldehyde as an aldehyde source, 100 mM glycine, 0.1 mM PLP, 10 mM magnesium chloride, and 100 mL of 200 mM Tris-hydrochloric acid buffer (pH 8.0). The resultant was subjected to reaction at 30° C. for 20 hours.

When formaldehyde was used as an aldehyde source, the yield was 90%. Also, when acetaldehyde was used as aldehyde source, the yield was 10%.

Example 5

(D-Serine Synthesis Reaction at a Formaldehyde Concentration of 100 mM)

The enzyme solutions (150 units each) subjected to ultrasonic disruption of the recombinant microorganisms produced in Example 1 were separately added to a substrate solution comprising 100 mL of 200 mM Tris-hydrochloric acid buffer (pH 8.0) containing 100 mM formaldehyde, 100 mM glycine, 0.1 mM PLP, and 10 mM magnesium chloride. The resultants were subjected to reaction at 30° C. for 20 hours. Table 1 shows the results.

TABLE 1 Reaction Host Plasmid yield DH5α pAcDTA1 90% pAcDTA2 80% pAcDTA3 72%

Example 6

(Production of D-Serine Deaminase-Deficient Escherichia coli)

The entire nucleotide sequence (GenBanak accession number: U00096) of genomic DNA of Escherichia coli is known to the public. Also, the amino acid sequence of Escherichia coli D-serine deaminase and the nucleotide sequence (GenBank accession number: J01603) of the gene thereof (hereafter to be abbreviated in some cases as dsdA) have already been reported. PCR was carried out using genomic DNA of Escherichia coli cell line W3110 (ATCC27325) as a template and oligonucleotides having the nucleotide sequences set forth in SEQ ID NOS: 9, 10, 11, and 12, which had been produced based on genetic information regarding a region in the vicinity of dsdA of genomic DNA of Escherichia coli cell line W3110. The obtained DNA fragments were digested with PstI and XbaI and with XbaI and KpnI, respectively, which are restriction enzymes. Thus, approximately 900-bp and 800-bp fragments of each DNA fragment were obtained. The resulting DNA fragments were mixed with fragments obtained by digesting a temperature-sensitive cloning vector pTH18cs1 (GenBank accession number: AB019610) (Hashimoto-Gotoh, T., Gene, 241, 185-191 (2000)) with PstI and KpnI, followed by ligation using a ligase. The resultant was transformed into a DH5α cell line at 30° C. Thus, a transformant that was able to grow on an LB agar plate containing 10 μg/ml of chloramphenicol was obtained. The obtained colony was cultured overnight at 30° C. in an LB liquid medium containing 10 μg/ml of chloramphenicol so that a plasmid was recovered from the obtained cell bodies. The obtained plasmid was digested with XbaI so as to be subjected to blunt-end treatment with T4DNA polymerase. Thereafter, the plasmid was ligated with a kanamycin-resistant gene derived from pUC4K plasmid (Pharmacia).

The thus obtained plasmid was transformed into Escherichia coli cell line W3110 (ATCC27325) at 30° C., followed by overnight culture at 30° C. on an LB agar plate containing 10 μg/ml of chloramphenicol and 50 μg/ml of kanamycin. Thus, a transformant was obtained. An LB liquid medium containing 50 μg/ml of kanamycin was inoculated with the obtained transformant, followed by overnight culture at 30° C. Next, the resultant was applied to an LB agar plate containing 50 μg/ml of kanamycin so as to obtain the culture cell bodies. Thus, colonies that were able to grow at 42° C. were obtained. The obtained colonies were cultured overnight at 30° C. in an LB liquid medium containing 50 μg/ml of kanamycin. The resultant was further applied to an LB agar plate containing 50 μg/ml of kanamycin so as to obtain colonies that were able to grow at 42° C.

100 colonies were randomly picked up from the colonies that appeared. Each of them was allowed to grow on an LB agar plate containing 50 μg/ml of kanamycin and on an LB agar plate containing 10 μg/ml of chloramphenicol. Then, chloramphenicol-sensitive clones that exclusively grow on an LB agar plate containing kanamycin were selected. Further, fragments (of approximately 3.0 kb) in the region in the vicinity of dsdA were amplified by PCR from chromosome DNAs of these clones of interest. Then, a cell line in which dsdA had been substituted with a kanamycin-resistant gene was selected. The obtained cell line was designated as a W3110dsdA-deficient cell line (hereafter to be abbreviated in some cases as ΔdsdA). Transformation was carried out using the plasmids produced in Example 1 so that cryopreservated cell bodies were produced as described above. Then, a similar reaction was carried out. As a result, substantially no D-serine degradation was confirmed.

Example 7

(Production of D-Serine with the Use of a Transformant MT-11016: Production without Addition of Mg)

Distilled water (53.1 g) was added to 7.5 g of glycine and 9.4 g of pyridoxal phosphate (0.026% by weight). The resultant was adjusted to pH 8.0 with sodium hydroxide. A cell suspension (corresponding to 1500 units in terms of activity) of MT-11016 obtained in Example 1 was added thereto. Then, 20.8 g of formaldehyde (20% by weight) was added thereto at a reaction temperature of 30° C. in a manner such that formaldehyde concentration in the reaction solution was quantified by the AHMT method (Eisei Kagaku (Journal of Health Science) (1976), Vol. 22, p. 39) as being between 50 mM and 300 mM. The pH of the reaction solution was adjusted to pH 8.0 with sodium hydroxide. The reaction yield after 72 hours reached 85%.

Example 8

(Production of D-Serine with the Use of a Transformant MT-11017: Production without Addition of Mg)

Distilled water (53.1 g) was added to 7.5 g of glycine and 9.4 g of pyridoxal phosphate (0.026% by weight). The resultant was adjusted to pH 8.0 with sodium hydroxide. A cell suspension (corresponding to 1500 units in terms of activity) of MT-11017 obtained in Example 1 was added thereto. Then, 20.8 g of formaldehyde (20% by weight) was added to the reaction solution at a reaction temperature of 30° C. by repeating cycles of addition of formaldehyde at a rate of 0.8 g/15 minutes for 15 minutes and discontinuation of the addition of formaldehyde for 45 minutes. The pH of the reaction solution was adjusted to pH 8.0 with sodium hydroxide during reaction. After 24 hours, the reaction yield of D-serine reached 95%.

Meanwhile, when formaldehyde was added at once so as to be subjected to reaction, the reaction yield was 20%.

Example 9

(Production of D-Serine with the Use of a Transformant Treated with Formaldehyde: Production without Addition of Mg)

Formaldehyde was added to a lysate of the frozen cell bodies of MT-11015 produced in Example 1 such that the lysate contained 100 mM formaldehyde, followed by mild agitation at 30° C. for 1 hour. During agitation, the pH was adjusted to 8.0 with sodium hydroxide. The resulting suspension of the cell bodies was subjected to the same reaction as that of Example 8. When formaldehyde treatment was not carried out, 2 mol % of L-serine was produced. When formaldehyde treatment was carried out, it was impossible to detect L-serine.

6N-hydrochloric acid was added to the above reaction solution such that the solution was adjusted to pH 4.1. Activated carbon (0.97 g; water content of 50%) was added thereto, followed by agitation at 60° C. for 1 hour. Activated carbon and cell body components were removed by filtration. Then, the filtrate was concentrated to 30 g. Isopropyl alcohol (13 g) was gradually added thereto, followed by mild agitation on ice for 1 hour. Thus, D-serine was allowed to deposit. The solution containing crystal deposits was filtrated. The crystal deposits were washed with 13 mL of cooled 40% isopropyl alcohol, followed by dehydration. The recovery rate was 60%, and white D-serine crystal was obtained. Glycine as a starting material was not detected. The optical purity of the crystal was 99.8% ee.

Example 10

[10-1] (Cloning of DTA of Xanthomonas and Vector Construction)

An LB medium (50 ml) was inoculated with Xanthomonas oryzae (IAM1657), which is obtainable from the Institute of Molecular and Cellular Biosciences at the University of Tokyo. After overnight culture at 30° C., harvest was carried out, followed by bacteriolysis using a lytic solution containing lysozyme (1 mg/ml). The resulting lysate was subjected to phenol treatment. Then, DNA was allowed to precipitate by ethanol precipitation in accordance with a usual method. The resulting DNA precipitate was recovered by spooling it onto a glass rod and washed so as to be used for PCR.

Primers used for PCR were oligonucleotides (obtained by custom synthesis from Hokkaido System Science Co., Ltd.) having the nucleotide sequences set forth in SEQ ID NOS: 13 and 14, respectively, which were designed based on a known DTA gene of Xanthomonas oryzae (GenBanak accession number: E05055). These primers had KpnI and HindIII restriction enzyme recognition sequences near the 5′ and 3′ ends, respectively.

With the use of 0.025 ml of a PCR reaction solution containing 6 ng/μl each of chromosome DNAs of the aforementioned microorganisms and 3 μM each of the aforementioned primers, PCR was carried out under the following conditions: denaturation at 96° C. for 1 minute, annealing at 55° C. for 30 seconds, and elongation reaction at 68° C. for 1 minute and 15 seconds for 35 reaction cycles.

The PCR reaction product and plasmid pUC18 (Takara Shuzo) were digested with KpnI and HindIII, followed by ligation using Ligation High (TOYOBO). Thereafter, the obtained recombinant plasmid was used for transformation of Escherichia coli DH5α. The transformed cell line was cultured in an LB agar medium containing 50 μg/ml of ampicillin (Am) and X-Gal (5-bromo-4-chloro-3-indolyl-β-D-galactoside). Thus, an Am-resistant transformed cell line that was formed into a white colony was obtained. A plasmid was extracted from the thus obtained transformed cell line. The nucleotide sequence of the DNA fragment that had been introduced into the plasmid was confirmed to be a sequence identical to the sequence of DTA of Xanthomonas oryzae in accordance with a usual method for base sequencing. The obtained expression plasmid was designated as pXDTA1.

[10-2] (Obtaining Escherichia coli Expressing DTA of the Genus Xanthomonas)

Escherichia coli W3110ΔdsdA was transformed by a usual method using pXDTA1. The obtained transformed cell line was designated as MT-11028.

In addition, Escherichia coli W3110ΔdsdA was transformed by a usual method using pAcDTA1, pAcDTA2, and pAcDTA3 obtained in Example 1. The obtained transformants were designated as MT-11015W, MT-11016W, and MT-11017W, respectively.

[10-3] (Obtaining Cell Bodies Via Jar Culture)

A LB medium (100 mL) containing 50 μg/ml of Am was inoculated with recombinant Escherichia coli (MT-11015W, MT-11016W, MT-11017W, and MT-11028) after being placed in a 500-mL baffled Erlenmeyer flask. This was followed by culture at 30° C. until OD660 reached 1.0.

Subsequently, culture was carried out using BMS10 with capacity of 10 L (produced by ABLE). Operations were carried out under the following culture conditions: agitation: 700 rpm; temperature: 30° C.; pH (maintained with NH₃): 7.2; aeration: 1 vvm; capacity: 5 L; and culture time: 48 hours. A medium used had a medium composition comprising 7 g of polypeptone (Dainippon Pharma), 0.09 g of ferrous sulfate heptahydrate, 1.5 g of ammonium sulfate, 2 g of magnesium sulfate hexahydrate, 2 g of monopotassium hydrogen phosphate, 2 g of dipotassium hydrogen phosphate, and 0.6 g of ADEKA NOL LG126 (Asahi Denka Kogyo K.K.) with respect to 1 L of water, unless specified.

Before inoculation, glucose was added, resulting in a glucose concentration of 20 g/L. Then, 50 mL of the culture solution in the aforementioned baffled Erlenmeyer flask was used for inoculation. After the glucose that had been added first became depleted under the aforementioned conditions, glucose was supplied at a variable rate (that resulted in less than 0.1 g/L of glucose) during the remaining time such that the total amount of glucose added was 200 g. Cell bodies were collected from the culture solution via centrifugation so as to be frozen at −20° C.

[10-4] (Restraining of Formation of L-Serine as a Byproduct from a Microorganism Treated with an Organic Solvent)

[Method for Measuring Enzyme Activity of Formation of L-Serine as a Byproduct]

Magnesium chloride hexahydrate (1.0 g) was added to 60 g of frozen cell bodies of MT-11028 (with a solid content percentage of approximately 10%). A variety of organic solvents were added thereto in a manner such that the resultant contained the solvents at given concentrations, followed by agitation at 35° C. for 1 hour.

Cell bodies (weighing 0.22 g as dry cell bodies) were taken from the above processed cell solution. The solution (9 g) used for enzyme activity measurement was added thereto, followed by agitation at 35° C. for 20 hours. Then, the ratio between L-serine produced and residual D-serine was measured. Table 2 collectively shows the results.

(Solution Used for L-Serine Production Activity Measurement)

D-serine (10.84 g) and PLP (6 mg) were dissolved in 0.5 M potassium phosphate buffer (pH 7.0) such that 100 g of the resultant was obtained.

TABLE 2 DSA Type of organic Concentration Optical purity residual solvent upon treatment of D-serine activity Water   93% 95% Isopropyl alcohol 20% by weight    96% 50% Benzaldehyde 5% by weight 97.5% 82% Dichloroethane 5% by weight 98.2% 103%  Formaldehyde 0.5% by weight   98.7% 46%

Example 11

(D-Serine Synthesis with the Use of Microorganisms Treated with an Organic Solvent)

Magnesium chloride hexahydrate (1.85 g) and 1.2 g of formaldehyde (37% by weight) were added to 83.4 g of wet cell bodies (with a solid content percentage of approximately 10%) obtained in Example 10. Water was added thereto such that the formaldehyde concentration was adjusted to 0.5%, followed by agitation at 35° C. for 1 hour.

Glycine (80 g), 4 g of magnesium chloride hexahydrate (35% by weight), and 3.1 g of formaldehyde (37% by weight) were added to 280 g of water. The pH of the resultant was adjusted to 7.5 with sodium hydroxide.

3.2 g of a PLP solution (0.38% by weight) was added thereto. Reaction was initiated by adding 30 g of the above cell bodies treated with an organic solvent as wet cell bodies. During reaction, formaldehyde was added when the pH became higher than 7.3 so that the pH was controlled at 7.3. The formaldehyde concentration during reaction was obtained by subtracting the amount of D-serine produced that was quantified by HPLC from the amount of formaldehyde added. The formaldehyde concentration in the reaction solution was controlled approximately between 80 mM and 100 mM. As a result of analysis of serine after the termination of reaction by HPLC, the yield relative to that of Gly was 95 mol % and the optical purity was 99.9% ee.

Example 12

(Example of Reaction with High Formaldehyde Concentration)

Glycine (80 g) and 4 g of magnesium chloride hexahydrate (35% by weight) were added to 280 g of water so as to be dissolved therein. Formaldehyde was added thereto such that the concentrations listed below were achieved, followed by control of pH at 7.5 with the use of sodium hydroxide. After the addition of 3.2 g of PLP (0.38% by weight), 30 g of frozen cell bodies obtained in Example 10 were added thereto so as to initiate reaction. When the pH reached 7.3 or more during reaction, formaldehyde was added such that pH was controlled at 7.3. Table 3 collectively shows the results.

TABLE 3 Formaldehyde Reac- Micro- concentration in reaction Optical tion organism solution purity yield Com- MT-11028 10 to 20 mM 96.5% 77.9% parative example Examples MT-11028 Approximately 150 mM 98.1% 98.0% Approximately 330 mM 99.8% 98.5% Approximately 410 mM 99.9% 96.6% Approximately 660 mM 99.9% 95.0% Approximately 1300 mM 99.9% 95.0% Approximately 2000 mM 99.9% 90.0% MT-11015W Approximately 410 mM 99.9% 89.7% MT-11016W Approximately 410 mM 99.8% 96.6% MT-11017W Approximately 410 mM 99.8% 90.5%

Example 13

[13-1] (Construction of Escherichia coli in which the glyA Gene is Destroyed and Production of DSA-Producing Bacteria)

The entire nucleotide sequence of Escherichia coli genomic DNA is known to the public (GenBanak accession number: U00096), Also, the amino acid sequence of Escherichia coli serine hydroxymethyltransferase and the nucleotide sequence (GenBank accession number: J01620) of the gene thereof (hereafter to be abbreviated in some cases as glyA) have already been reported. PCR was carried out using genomic DNA of Escherichia coli cell line W3110 (ATCC27325) as a template and oligonucleotides having the nucleotide sequences set forth in SEQ ID NOS: 15, 16, 17, and 18, which were produced based on genetic information regarding a region in the vicinity of glyA of genomic DNA of Escherichia coli cell line W3110. The obtained DNA fragments were digested with BamHI and PstI and with PstI and HindIII, respectively, which are restriction enzymes. Thus, approximately 850 bp and 750 bp fragments of each DNA fragment were obtained. The resulting DNA fragments were mixed with fragments obtained by digesting a temperature-sensitive cloning vector pTH18cs1 (GenBank accession number: AB019610) (Hashimoto-Gotoh, T., Gene, 241, 185-191 (2000)) with BamHI and HindIII, followed by ligation using a ligase. The resultant was transformed into a DH5α cell line at 30° C. Thus, a transformant that was able to grow on an LB agar plate containing 10 μg/ml of chloramphenicol was obtained. The obtained colony was cultured overnight at 30° C. in an LB liquid medium containing 10 μg/ml of chloramphenicol so that a plasmid was recovered from the obtained cell bodies. The recovered plasmid was digested with PstI so as to be subjected to blunt-end treatment with T4DNA polymerase. Thereafter, the plasmid was ligated with a tetracycline-resistant gene derived from transposon Tn10.

The thus obtained plasmid was transformed into Escherichia coli W3110dsdA-deficient cell line at 30° C., followed by overnight culture at 30° C. on an LB agar plate containing 10 μg/ml of chloramphenicol and 50 μg/ml of tetracycline. Thus, a transformant was obtained. An LB liquid medium containing 50 μg/ml of tetracycline was inoculated with the obtained transformant, followed by overnight culture at 30° C. Next, the resultant was applied to an LB agar plate containing 50 μg/ml of tetracycline so as to obtain the culture cell bodies. Thus, colonies that grow at 42° C. were obtained. The obtained colonies were cultured overnight in an LB liquid medium containing 50 μg/ml of tetracycline at 30° C. The resultant was further applied to an LB agar plate containing 50 μg/ml of tetracycline so as to obtain colonies that grow at 42° C.

100 colonies were randomly picked up from the colonies that appeared. Each of them was allowed to grow on an LB agar plate containing 50 μg/ml of tetracycline and on an LB agar plate containing 10 μg/ml of chloramphenicol. Then, chloramphenicol-sensitive clones that exclusively grow on an LB agar plate containing tetracycline were selected. Further, fragments (of approximately 3.6 kbp) in the region in the vicinity of glyA were amplified by PCR from chromosome DNAs of these clones of interest. Then, a cell line in which glyA had been substituted with a tetracycline-resistant gene was selected. The obtained cell line was designated as a W3110dsdA/glyA-deficient cell line.

[13-2] (Effects of Escherichia coli in which the glyA Gene is Destroyed)

This Escherichia coli was transformed with plasmid pXDTA1, followed by culture in the same manner as that used in Example 10. Note that 20 mg/L of glycine was added in the case of flask culture and 2 g/L of glycine was added in the case of culture in a fermenter. During culture, glycine used was added at several different times.

L-serine production activity was examined in the same manner as that used in Example 9. D-serine optical purity was 97%.

Example 14

(Effects of Metal Salts)

300 mM EDTA (3.5 g; pH 7.5) was added to 100 g of frozen cell bodies of MT-11028 obtained in Example 10, followed by agitation at 4° C. for 1 hour. The resulting suspension (10 g) was suspended in 10 g of 0.5 M potassium phosphate buffer (pH 7.0) containing 20 mM each of manganese chloride, zinc sulfate, cobalt chloride, nickel chloride, calcium chloride, and ferrous chloride, followed by agitation at 4° C. for 1 hour.

Next, formaldehyde was added to the above suspension so as to account for 0.5% of the resultant, followed by agitation at 35° C. for 1 hour. Cell bodies (weighing 0.22 g as dry cell bodies) were taken from the above processed cell solution. The solution (9 g) used for enzyme activity measurement described in Example 10 was added thereto, followed by agitation at 35° C. for 20 hours. Then, the ratio between L-serine produced and residual D-serine was measured.

In a case in which a metal salt was used, optical purity of D-serine was 96% or more. In addition, 50% or more of the activity of the enzyme synthesizing D-serine from formaldehyde and glycine was maintained compared with the activity before organic solvent treatment, even in a case in which a metal salt was used.

Example 15

(Method for Improving Optical Purity Using L-Serine-Deaminase-Expressing Escherichia coli)

An LB medium (50 ml) was inoculated with Escherichia coli cell line K-12. After overnight culture at 30° C., harvest was carried out, followed by bacteriolysis using a lytic solution containing lysozyme (1 mg/ml). The resulting lysate was subjected to phenol treatment. Then, DNA was allowed to precipitate by ethanol precipitation in accordance with a usual method. The resulting DNA precipitate was recovered by spooling it onto a glass rod and washed so as to be used for PCR.

Primers used for PCR were oligonucleotides (obtained by custom synthesis from Hokkaido System Science Co., Ltd.) having nucleotide sequences set forth in SEQ ID NOS: 19 and 20, respectively, which were designed based on the known L-serine deaminase gene of Escherichia coli (GenBanak accession number: M28695). These primers had EcoRI and HindIII restriction enzyme recognition sequences near the 5′ and 3′ ends, respectively.

With the use of 0.025 ml of a PCR reaction solution containing 6 ng/μl each of chromosome DNAs of the aforementioned microorganisms and 3 μM each of the primers, PCR was carried out under the following conditions: denaturation at 96° C. for 1 minute, annealing at 55° C. for 30 seconds, and elongation reaction at 68° C. for 1 minute and 30 seconds for 35 reaction cycles.

The PCR reaction product and plasmid pUC18 (Takara Shuzo) were digested with EcoRI and HindIII, followed by ligation using Ligation High (TOYOBO). Thereafter, the obtained recombinant plasmid was used for transformation of Escherichia coli DH5α. The transformed cell line was cultured in an LB agar medium containing 50 μg/ml of ampicillin (Am) and X-Gal (5-bromo-4-chloro-3-indolyl-β-D-galactoside). Thus, an Am-resistant transformed cell line that was formed into a white colony was obtained. A plasmid was extracted from the thus obtained transformed cell line. In accordance with a usual method for base sequencing, the nucleotide sequence of the DNA fragment that had been introduced into the plasmid was confirmed to be identical to the sequence of a known Escherichia coli L-serine deaminase. The obtained expression plasmid was designated as pSDA1.

The Escherichia coli W3110dsdA/glyA-deficient cell line was transformed by a usual method using pSDA1. The obtained transformant was cultured in a fermenter in the same manner as that used in Example 13.

In the same manner as that used for the as comparative example in Example 12, reaction was carried out by adding 10 g of the aforementioned cell bodies to a reaction solution. The reaction solution was analyzed by HPLC. Thus, optical purity of D-serine in the reaction solution was found to be 99.9%.

All publications, patents, and patent applications cited herein are incorporated herein by reference in their entirety.

INDUSTRIAL APPLICABILITY

The present invention is useful as a method for producing D-serine from glycine and formaldehyde. In addition, D-serine obtained by the production method of the present invention is useful, for example, as a medicine intermediate of a starting material of D-cycloserine that is useful as an antituberculous agent.

DRAWINGS

FIG. 1

-   M: Marker -   1: MT-11015 Cell disruption solution -   2: MT-11015 Cell disruption residue -   3: MT-11016 Cell disruption solution -   4: MT-11016 Cell disruption residue -   5: MT-11017 Cell disruption solution -   6: MT-11017 Cell disruption residue

FIG. 2

-   M: Molecular weight marker -   1: Solution subjected to ultrasonic disruption -   3: Ion exchange purification (Q XL) -   3: Hydrophobic chromatography purification (Phenyl FF) 

The invention claimed is:
 1. A method for producing D-serine, wherein D-serine is synthesized by allowing glycine to react with formaldehyde in the presence of a microorganism having activity of synthesizing D-serine from glycine and formaldehyde or a treated product thereof, wherein the microorganism is an isolated host cell transformed with a recombinant expression vector encoding an enzyme having activity of synthesizing D-serine from glycine and formaldehyde, the host cell being selected from the group consisting of Escherichia coli and yeasts, and the method comprising one or more of the following (i), (ii), and (iii) whereby formation of L-serine as a byproduct in a reaction solution is restrained such that L-serine accounts for 1.5 mol % or less relative to D-serine during the reaction: (i) allowing a microorganism having activity of synthesizing D-serine from glycine and formaldehyde to be subjected to an organic solvent treatment or heat treatment or both; (ii) controlling formaldehyde concentration in a reaction solution a) to 2M or less in a case in which an organic solvent treatment or heat treatment or both are/is carried out by the method (i) above and b) to from 330 mM to 2M inclusive in a case in which an organic solvent treatment or heat treatment or both are/is not carried out; and (iii) adding a microorganism comprising an enzyme having an L-serine deaminase activity to a reaction solution.
 2. The production method according to claim 1, wherein the organic solvent is at least one selected from the group consisting of formaldehyde, benzaldehyde, dichloroethane, and isopropyl alcohol.
 3. The production method according to claim 1 or claim 2, wherein the organic solvent treatment or heat treatment or both are/is carried out in the presence of divalent metal ions.
 4. The production method according to claim 3, wherein the divalent metals are one or more types of metals selected from the group consisting of magnesium, manganese, zinc, nickel, cobalt, and iron.
 5. The production method according to claim 1, wherein the microorganism has activity of synthesizing D-serine from glycine and formaldehyde in a reaction solution having a high formaldehyde concentration of 410 mM.
 6. The production method according to claim 1, wherein the host cell is Escherichia coli.
 7. The production method according to claim 1, comprising (i) allowing a microorganism having activity of synthesizing D-serine from glycine and formaldehyde to be subjected to an organic solvent treatment or heat treatment or both.
 8. The production method according to claim 1, comprising (ii) controlling formaldehyde concentration in a reaction solution a) to 2M or less in a case in which an organic solvent treatment or heat treatment or both are/is carried out by the method (i) above and b) to from 330 mM to 2M inclusive in a case in which an organic solvent treatment or heat treatment or both are/is not carried out.
 9. The production method according to claim 1, comprising (iii) adding a microorganism comprising an enzyme having an L-serine deaminase activity to a reaction solution. 